Palm oil fractionation process

107224 Pushparajah, E.; 108427 Rajadurai, M. eds.; 10819 Incorporated Society of Planters, Kuala Lumpur (Malasia); 14918 N.V. Extraction De Smet S.A., Edegem (Bélgica); 15747 Palm Oil Research Inst. of Malaysia, Kuala Lumpur (Malasia); 35748 International Conference on Palm Oil Product Technology in the Eighties Kuala Lumpur (Malasia) 22-24 Jun 1981

$Palm oil fractionation process$

Palm oil fractionation process

The process described called 'superfluid fractionation' will produce a liquid palm oil fraction with an iodine value above 75. The liquid fraction has a good stability to the cold test. This is due to: (1) The selectivity regarding triglycerides of the disaturated-monounsaturated type (S24) and monosaturated-diunsaturated type (SU2) is better than in both the dry fractionation and the detergent fractionation. (2) The distribution of palm oil triglycerides when using the superfluid process is more favourable for a good separation of same triglycerides. Due to interesterification and the use of a selective solvent (Hexane), it is possible to facilitate the separation of these triglycerides and to obtain a minimum percentage of disaturated-monounsaturated triglycerides (S2U) in the liquid fraction

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Main Authors:	107224 Pushparajah, E., 108427 Rajadurai, M. eds., 10819 Incorporated Society of Planters, Kuala Lumpur (Malasia), 14918 N.V. Extraction De Smet S.A., Edegem (Bélgica), 15747 Palm Oil Research Inst. of Malaysia, Kuala Lumpur (Malasia), 35748 International Conference on Palm Oil Product Technology in the Eighties Kuala Lumpur (Malasia) 22-24 Jun 1981
Format:	biblioteca
Published:	Kuala Lumpur (Malasia) 1983
Subjects:	FRACCION FLUIDA, FRACCIONAMIENTO SUPERFLUIDO, ELAEIS GUINEENSIS, ACEITES DE PALMAS, PROCESAMIENTO, ACIDOS GRASOS, GLICERIDOS, COMPOSICION, PROPIEDADES FISICO-QUIMICAS,
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id	KOHA-OAI-BVE:40404
record_format	koha
spelling	KOHA-OAI-BVE:404042020-02-03T21:03:12ZPalm oil fractionation processPalm oil product technology in the eighties; proceedings 107224 Pushparajah, E. 108427 Rajadurai, M. eds. 10819 Incorporated Society of Planters, Kuala Lumpur (Malasia) 14918 N.V. Extraction De Smet S.A., Edegem (Bélgica) 15747 Palm Oil Research Inst. of Malaysia, Kuala Lumpur (Malasia) 35748 International Conference on Palm Oil Product Technology in the Eighties Kuala Lumpur (Malasia) 22-24 Jun 1981 Kuala Lumpur (Malasia)1983The process described called 'superfluid fractionation' will produce a liquid palm oil fraction with an iodine value above 75. The liquid fraction has a good stability to the cold test. This is due to: (1) The selectivity regarding triglycerides of the disaturated-monounsaturated type (S24) and monosaturated-diunsaturated type (SU2) is better than in both the dry fractionation and the detergent fractionation. (2) The distribution of palm oil triglycerides when using the superfluid process is more favourable for a good separation of same triglycerides. Due to interesterification and the use of a selective solvent (Hexane), it is possible to facilitate the separation of these triglycerides and to obtain a minimum percentage of disaturated-monounsaturated triglycerides (S2U) in the liquid fractionThe process described called 'superfluid fractionation' will produce a liquid palm oil fraction with an iodine value above 75. The liquid fraction has a good stability to the cold test. This is due to: (1) The selectivity regarding triglycerides of the disaturated-monounsaturated type (S24) and monosaturated-diunsaturated type (SU2) is better than in both the dry fractionation and the detergent fractionation. (2) The distribution of palm oil triglycerides when using the superfluid process is more favourable for a good separation of same triglycerides. Due to interesterification and the use of a selective solvent (Hexane), it is possible to facilitate the separation of these triglycerides and to obtain a minimum percentage of disaturated-monounsaturated triglycerides (S2U) in the liquid fractionFRACCION FLUIDAFRACCIONAMIENTO SUPERFLUIDOELAEIS GUINEENSISACEITES DE PALMASPROCESAMIENTOACIDOS GRASOSGLICERIDOSCOMPOSICIONPROPIEDADES FISICO-QUIMICASURN:ISBN:9679949001
institution	IICA
collection	Koha
country	Costa Rica
countrycode	CR
component	Bibliográfico
access	En linea Fisico
databasecode	cat-sibiica
tag	biblioteca
region	America Central
libraryname	Sistema de Bibliotecas IICA/CATIE
topic	FRACCION FLUIDA FRACCIONAMIENTO SUPERFLUIDO ELAEIS GUINEENSIS ACEITES DE PALMAS PROCESAMIENTO ACIDOS GRASOS GLICERIDOS COMPOSICION PROPIEDADES FISICO-QUIMICAS FRACCION FLUIDA FRACCIONAMIENTO SUPERFLUIDO ELAEIS GUINEENSIS ACEITES DE PALMAS PROCESAMIENTO ACIDOS GRASOS GLICERIDOS COMPOSICION PROPIEDADES FISICO-QUIMICAS
spellingShingle	FRACCION FLUIDA FRACCIONAMIENTO SUPERFLUIDO ELAEIS GUINEENSIS ACEITES DE PALMAS PROCESAMIENTO ACIDOS GRASOS GLICERIDOS COMPOSICION PROPIEDADES FISICO-QUIMICAS FRACCION FLUIDA FRACCIONAMIENTO SUPERFLUIDO ELAEIS GUINEENSIS ACEITES DE PALMAS PROCESAMIENTO ACIDOS GRASOS GLICERIDOS COMPOSICION PROPIEDADES FISICO-QUIMICAS 107224 Pushparajah, E. 108427 Rajadurai, M. eds. 10819 Incorporated Society of Planters, Kuala Lumpur (Malasia) 14918 N.V. Extraction De Smet S.A., Edegem (Bélgica) 15747 Palm Oil Research Inst. of Malaysia, Kuala Lumpur (Malasia) 35748 International Conference on Palm Oil Product Technology in the Eighties Kuala Lumpur (Malasia) 22-24 Jun 1981 Palm oil fractionation process
description	The process described called 'superfluid fractionation' will produce a liquid palm oil fraction with an iodine value above 75. The liquid fraction has a good stability to the cold test. This is due to: (1) The selectivity regarding triglycerides of the disaturated-monounsaturated type (S24) and monosaturated-diunsaturated type (SU2) is better than in both the dry fractionation and the detergent fractionation. (2) The distribution of palm oil triglycerides when using the superfluid process is more favourable for a good separation of same triglycerides. Due to interesterification and the use of a selective solvent (Hexane), it is possible to facilitate the separation of these triglycerides and to obtain a minimum percentage of disaturated-monounsaturated triglycerides (S2U) in the liquid fraction
format
topic_facet	FRACCION FLUIDA FRACCIONAMIENTO SUPERFLUIDO ELAEIS GUINEENSIS ACEITES DE PALMAS PROCESAMIENTO ACIDOS GRASOS GLICERIDOS COMPOSICION PROPIEDADES FISICO-QUIMICAS
author	107224 Pushparajah, E. 108427 Rajadurai, M. eds. 10819 Incorporated Society of Planters, Kuala Lumpur (Malasia) 14918 N.V. Extraction De Smet S.A., Edegem (Bélgica) 15747 Palm Oil Research Inst. of Malaysia, Kuala Lumpur (Malasia) 35748 International Conference on Palm Oil Product Technology in the Eighties Kuala Lumpur (Malasia) 22-24 Jun 1981
author_facet	107224 Pushparajah, E. 108427 Rajadurai, M. eds. 10819 Incorporated Society of Planters, Kuala Lumpur (Malasia) 14918 N.V. Extraction De Smet S.A., Edegem (Bélgica) 15747 Palm Oil Research Inst. of Malaysia, Kuala Lumpur (Malasia) 35748 International Conference on Palm Oil Product Technology in the Eighties Kuala Lumpur (Malasia) 22-24 Jun 1981
author_sort	107224 Pushparajah, E.
title	Palm oil fractionation process
title_short	Palm oil fractionation process
title_full	Palm oil fractionation process
title_fullStr	Palm oil fractionation process
title_full_unstemmed	Palm oil fractionation process
title_sort	palm oil fractionation process
publisher	Kuala Lumpur (Malasia)
publishDate	1983
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Palm oil fractionation process

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